JP2001278715A - Silver-supporting antimicrobial agent for water treatment and its application method - Google Patents
Silver-supporting antimicrobial agent for water treatment and its application methodInfo
- Publication number
- JP2001278715A JP2001278715A JP2000132952A JP2000132952A JP2001278715A JP 2001278715 A JP2001278715 A JP 2001278715A JP 2000132952 A JP2000132952 A JP 2000132952A JP 2000132952 A JP2000132952 A JP 2000132952A JP 2001278715 A JP2001278715 A JP 2001278715A
- Authority
- JP
- Japan
- Prior art keywords
- silver
- zeolite
- water treatment
- supporting
- supported
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 43
- 238000011282 treatment Methods 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims description 16
- 239000004599 antimicrobial Substances 0.000 title abstract 3
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract description 121
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims abstract description 119
- 239000004332 silver Substances 0.000 claims abstract description 119
- 229910052709 silver Inorganic materials 0.000 claims abstract description 119
- 239000010457 zeolite Substances 0.000 claims abstract description 117
- 229910021536 Zeolite Inorganic materials 0.000 claims abstract description 115
- 238000010828 elution Methods 0.000 claims abstract description 25
- 239000000463 material Substances 0.000 claims abstract description 17
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 239000013078 crystal Substances 0.000 claims abstract description 10
- 238000000926 separation method Methods 0.000 claims abstract description 7
- 239000003242 anti bacterial agent Substances 0.000 claims description 20
- 239000002245 particle Substances 0.000 abstract description 17
- 239000000243 solution Substances 0.000 abstract description 9
- 239000007864 aqueous solution Substances 0.000 abstract description 5
- 230000001105 regulatory effect Effects 0.000 abstract 2
- 239000000047 product Substances 0.000 description 29
- 239000008399 tap water Substances 0.000 description 18
- 235000020679 tap water Nutrition 0.000 description 18
- 239000010410 layer Substances 0.000 description 12
- 238000012360 testing method Methods 0.000 description 12
- 238000001179 sorption measurement Methods 0.000 description 11
- 238000004519 manufacturing process Methods 0.000 description 7
- 229920003002 synthetic resin Polymers 0.000 description 7
- 239000000057 synthetic resin Substances 0.000 description 7
- 230000000844 anti-bacterial effect Effects 0.000 description 6
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 description 6
- 239000011230 binding agent Substances 0.000 description 5
- 238000007922 dissolution test Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000010419 fine particle Substances 0.000 description 4
- 238000010304 firing Methods 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 239000011435 rock Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 description 3
- 238000000673 graphite furnace atomic absorption spectrometry Methods 0.000 description 3
- 238000011068 loading method Methods 0.000 description 3
- 229910052863 mullite Inorganic materials 0.000 description 3
- 229910001961 silver nitrate Inorganic materials 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 2
- 239000000440 bentonite Substances 0.000 description 2
- 229910000278 bentonite Inorganic materials 0.000 description 2
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 2
- 229910052801 chlorine Inorganic materials 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- JYIMWRSJCRRYNK-UHFFFAOYSA-N dialuminum;disodium;oxygen(2-);silicon(4+);hydrate Chemical class O.[O-2].[O-2].[O-2].[O-2].[O-2].[O-2].[Na+].[Na+].[Al+3].[Al+3].[Si+4] JYIMWRSJCRRYNK-UHFFFAOYSA-N 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 229910052680 mordenite Inorganic materials 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 230000002265 prevention Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 241000195493 Cryptophyta Species 0.000 description 1
- 241000588724 Escherichia coli Species 0.000 description 1
- 241000589248 Legionella Species 0.000 description 1
- 208000007764 Legionnaires' Disease Diseases 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000007872 degassing Methods 0.000 description 1
- 230000006806 disease prevention Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 230000000855 fungicidal effect Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 238000004255 ion exchange chromatography Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 235000019645 odor Nutrition 0.000 description 1
- -1 pools Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Agricultural Chemicals And Associated Chemicals (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、水処理用銀担持抗菌剤
とその使用方法に関し、特に、粒子の大きさが大きな担
体としての素材にPH5以下にならないような処理液中
で直接銀を担持させることによりその製造工程を著しく
簡素化するとともに、微粒子の銀ゼオライトを使用した
従来の製品より性能が優れた水処理用銀担持抗菌剤とそ
の使用方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an antibacterial silver-carrying agent for water treatment and a method for using the same. The present invention relates to a silver-carrying antibacterial agent for water treatment and a method of using the same, which significantly simplifies the production process by having the silver zeolite supported and has higher performance than conventional products using fine-particle silver zeolite.
【0002】[0002]
【従来の技術】水の需要の増大とともに水質向上が求め
られ、より無害で適切な水処理法が望まれる。なかでも
銀ゼオライトのすぐれた抗菌性を活かして水処理用抗菌
剤として使えるようにすることが求められ開発もなされ
ている。現在使用されている銀ゼオライトの粒子の大き
さはミクロン単位のものである。しかしながら、水処理
用としては現在の銀ゼオライトの粒子の大きさを以てし
ては水の中で固液分離ができないので銀ゼオライトを水
溶液に直接投入することはできない。そのためにこのよ
うな微粒子の銀ゼオライトはこれを固めて成形体として
用いる必要がある。しかし、ゼオライト自体には自己結
合性がないためにバインダを添加して成形する。その単
位重量当たりの抗菌性能はバインダの分だけもとの銀ゼ
オライト粉末よりも低下することになるが現在のところ
成形体として使用する利点の方が大きいためにこの方法
が採用されている。現在業界が開発しているものには次
のものがある。 (1) 粒子径1〜2μのA型ゼオライトを硝酸銀水溶
液との接触で銀含有量2〜2.5%の銀ゼオライトを
得、この銀ゼオライトを合成樹脂に1〜10%添加、成
形する。粒子の大きさは0.5〜2.0mm乃至5〜1
0mmとしている。この開発目的は塩素を除去した水道
水を水槽で無菌状態で貯水することであり、銀ゼオライ
トを10%添加し成形した樹脂を水の10%の量を以て
投入した場合いい成績を収めたとしている(特開平4−
294782)。 (2)(1)と同様にまづA型ゼオライトを担体として
銀担持量2〜2.5%の銀ゼオライトを作り、これに等
量のバインダCaCO3を混合し、さらにこれに対し3
0%のベントナイトを添加し、湿式混和ののち押出して
ペレットとする。ペレットを乾燥後、550゜Cで3時
間焼成する。製品の大きさは1/16吋で銀含有量は
0.89%である(特公昭63−28402)。 (3) 合成樹脂の3〜5mm大きさの粒子をミキサー
で高速回転し、溶融が始まった時点でトルエンをミキサ
ーに投入し、これに銀ゼオライトの微粉をふりかけ合成
樹脂の粒子の表面に直接銀ゼオライトをコーティングし
たもの。この開発目的は、銀ゼオライトをそのまま直接
水に投入することは好ましくないこと、と銀ゼオライト
を合成樹脂に混合して成形加工した水処理用抗菌剤の場
合抗菌機能が表面のみに限定されること、としている
(特開平5−176976)。2. Description of the Related Art As the demand for water increases, the quality of water is required to be improved, and a more harmless and appropriate water treatment method is desired. Above all, it has been required and developed that silver zeolite can be used as an antibacterial agent for water treatment by taking advantage of its excellent antibacterial properties. Currently used silver zeolite particles are on the order of microns. However, for water treatment, silver zeolite cannot be directly introduced into an aqueous solution because solid-liquid separation cannot be performed in water depending on the current silver zeolite particle size. Therefore, it is necessary to solidify such fine particles of silver zeolite and use it as a compact. However, since zeolite itself has no self-bonding property, it is molded by adding a binder. The antibacterial performance per unit weight is lower than that of the original silver zeolite powder by the amount of the binder, but at present, this method is adopted because the advantage of using it as a molded article is greater. Some of the things the industry is currently developing include: (1) A type zeolite having a particle size of 1 to 2 μm is contacted with an aqueous silver nitrate solution to obtain a silver zeolite having a silver content of 2 to 2.5%, and the silver zeolite is added to a synthetic resin at 1 to 10% and molded. Particle size is 0.5 to 2.0 mm to 5 to 1
0 mm. The purpose of this development is to store tap water from which chlorine has been removed under aseptic conditions in a water tank. It is said that good results were obtained when 10% of silver zeolite was added and the molded resin was added in an amount of 10% of water. (JP-A-4-
294782). (2) In the same manner as in (1), a silver zeolite having a silver loading of 2 to 2.5% was prepared using A-type zeolite as a carrier, and an equal amount of a binder CaCO 3 was mixed with the zeolite.
Add 0% bentonite, wet mix and extrude into pellets. After drying, the pellets are fired at 550 ° C. for 3 hours. The size of the product is 1/16 inch and the silver content is 0.89% (JP-B-63-28402). (3) The synthetic resin particles having a size of 3 to 5 mm are rotated at a high speed by a mixer, and when melting starts, toluene is charged into the mixer, and fine powder of silver zeolite is sprinkled on the mixture, and silver is directly applied to the surface of the synthetic resin particles. One coated with zeolite. The purpose of this development is that it is not preferable to put silver zeolite directly into water as it is, and in the case of an antibacterial agent for water treatment formed by mixing silver zeolite with synthetic resin, the antibacterial function is limited only to the surface. (Japanese Patent Application Laid-Open No. 5-176976).
【0003】[0003]
【発明が解決しようとする課題】以上のように現状にお
いては、或る大きさの粒子を得るために微粒子の銀ゼオ
ライトをもとにして イ)湿式混和、押出し、乾燥、焼成の工程を経て成形す
る方法 ロ)合成樹脂と混合し、射出成形機で成形する方法 がとられている。本発明者は現在行われているイ)、
ロ)のような製法、即ち、まづ銀ゼオライトを作り、こ
れをバインダに加え、或いは合成樹脂に混合して成形す
るといった工程を避け、直接粒子の大きなゼオライトの
成形品、或いは天然ゼオライトの破砕したものに対して
簡単に銀の担持を行うことに成功した。今回開発した方
法は、素材である任意の大きさのゼオライト粒子又はゼ
オライト系加工品にゼオライトの結晶構造を破壊しない
程度のPHを示す処理液中で直接銀を担持させるもので
ある。直径2〜3mmの大きさの粒子はもとより、これ
よりさらに大きなゼオライト粒子やゼオライト系加工品
等に銀担持が可能であり、その製造工程が著しく簡素化
され、同時に上記イ)、ロ)の製品よりはるかに性能が
優れた水処理用抗菌剤を作ることができた。そこで水処
理用として固液分離可能な任意の大きさのゼオライト粒
子又はゼオライト系加工品に、ゼオライトの結晶構造を
破壊しない程度のPHを示す処理液中で直接銀を担持さ
せた水処理用銀担持抗菌剤を提供することを本発明の第
1の課題とする。そのような素材に直接銀を担持させた
銀担持材のみで、又は銀担持材と銀無担持材との組み合
わせによって銀の溶出濃度の調節を可能とした水処理用
銀担持抗菌剤の使用方法を提供することを本発明の第2
の課題とする。銀を担持する担体としては、天然ゼオラ
イト原石、天然ゼオライトを加工して球状、円柱状、柱
状、円筒状等にしたもの、A型ゼオライト系成形体、A
型ゼオライトを原料にして作った焼成品、形状としては
球状、柱状、円筒状、コイン状薄片、シート状等であ
り、平成7年特許第255731号に記載の人工ゼオラ
イト系成形体、その焼成品等がある。As described above, in the present circumstances, in order to obtain particles of a certain size, fine particles of silver zeolite are used to obtain particles of a certain size. Method of molding b) A method of mixing with a synthetic resin and molding with an injection molding machine is used. The present inventor is currently conducting a),
(2) Avoid the process of first preparing silver zeolite, adding it to a binder, or mixing it with a synthetic resin and molding it, and crushing zeolite molded products with large particles or natural zeolite. We succeeded in carrying silver easily on the sample. In the method developed this time, silver is directly supported on a zeolite particle or zeolite-based processed product of an arbitrary size, which is a raw material, in a processing solution having a pH that does not destroy the zeolite crystal structure. Not only particles having a diameter of 2 to 3 mm, but also larger zeolite particles and zeolite-based processed products can be loaded with silver, and the production process is greatly simplified, and at the same time, the products of the above a) and b) An antibacterial agent for water treatment with much better performance could be made. Therefore, silver for water treatment, in which silver is directly supported on a zeolite particle or zeolite-based processed product of any size capable of solid-liquid separation for water treatment, in a treatment liquid having a pH that does not destroy the crystal structure of zeolite, It is a first object of the present invention to provide a supported antibacterial agent. A method for using a silver-supported antibacterial agent for water treatment that enables the adjustment of silver elution concentration by using only a silver-supporting material in which silver is directly supported on such a material or by combining a silver-supporting material and a silver-free material. Providing the second aspect of the present invention.
Subject. As a carrier for supporting silver, a natural zeolite ore, a natural zeolite processed into spherical, cylindrical, columnar, cylindrical, etc., an A-type zeolite-based molded product, A
A fired product made from a zeolite as a raw material, the shape of which is spherical, columnar, cylindrical, coin-shaped flake, sheet, etc., and an artificial zeolite-based molded product described in 1995 Patent No. 2555731, and a fired product thereof Etc.
【0004】[0004]
【課題を解決するための手段】本発明は、水処理用とし
て固液分離可能な任意の大きさのゼオライト粒子又はゼ
オライト系加工品に、ゼオライトの結晶構造を破壊しな
い程度のPHを示す処理液中で直接銀を担持させてなる
水処理用銀担持抗菌剤である。本発明はまた、水処理用
として固液分離可能な任意の大きさのゼオライト粒子又
はゼオライト系加工品に、ゼオライトの結晶構造を破壊
しない程度のPHを示す処理液中で直接銀を担持させた
銀担持材のみで、又は銀担持材と銀無担持材との組み合
わせによって銀の溶出濃度の調節を可能としてなる水処
理用銀担持抗菌剤の使用方法である。SUMMARY OF THE INVENTION The present invention provides a treatment liquid having a pH that does not destroy the zeolite crystal structure in zeolite particles or zeolite-based products of any size that can be separated into solids and liquids for water treatment. It is a silver-supported antibacterial agent for water treatment in which silver is directly supported in water. According to the present invention, silver is directly supported on a zeolite particle or zeolite-based processed product of any size capable of solid-liquid separation for water treatment in a processing solution having a pH that does not destroy the crystal structure of zeolite. This is a method of using a silver-carrying antibacterial agent for water treatment, which makes it possible to adjust the elution concentration of silver using only a silver-carrying material or a combination of a silver-carrying material and a silver-free material.
【0005】[0005]
【作用】微粒子の合成ゼオライトに銀を担持させる方法
を止めて、実施例に示すように水処理用抗菌剤として使
用することのできる大きさのゼオライト系粒子や成形ゼ
オライト系粒子に対して直接銀を担持することを試み
た。銀を担持する担体として天然ゼオライト破砕品、A
型ゼオライト系棒状成形品(直径1.5mm)、A型ゼ
オライト系コイン状成形品(径25mm、厚さ2〜3m
m)、その他一定の大きさを有するムライト系成形品等
を選んだ。これらいずれの試料についても良好な結果を
得た。即ち、 となった。A型ゼオライト系棒状成形品については、水
道水を用いてSV5及びSV20でカラム溶出試験、銀
の溶出濃度の調節試験、ビーカーによる長時間の溶出試
験を行った結果、溶出の安定性及び永続性を確認した。
天然ゼオライトについては国内に豊富に存在し安価であ
るが、従来、銀担持量が5mg−Ag/g−Zにとどま
り、抗菌剤としては成功していない。しかし、今回福島
県産モルデナイト系天然ゼオライトの原岩を破砕して本
発明のやり方で銀を担持させたところゼオライト1g当
たりAg145mgを担持した。さらにこれら銀ゼオラ
イトを用いてカラム溶出試験を行い、三群のカラムを準
備し銀の溶出、銀の溶出濃度の調節を試験した結果、銀
を担持する天然ゼオライトは水処理用抗菌剤として、合
成A型ゼオライト系成形品とともに活用できる目安がつ
いたものと考える。また、製造工程が著しく簡略化され
たため生産原価を安くすることが可能となる。A型ゼオ
ライトは結晶格子中に含まれるアルミニウムの濃度が高
くイオン交換容量が高くて銀担持力が大である反面、耐
酸性が低く、PH5以下の溶液に浸漬すると結晶構造が
崩壊してしまう。従って、本発明の水処理用抗菌剤とし
ての銀担持ゼオライトの製法の重要な特徴は、銀担持用
処理液の濃度がPH5以下とならないようにするととも
にゼオライト1g当たりの水溶液の量を従来のものより
極度に増量したことである。以下、従来品との比較を示
す。 このようにゼオライト1g当たりの水溶液の量を従来の
ものより極度に増量した結果、銀担持用処理液の濃度を
PH5以下に落とすことがなく、ゼオライト1g当たり
の銀担持量及び、ゼオライト1g当たりの担持した銀の
重量%は上記のとおりとなった。本発明の水処理用銀担
持抗菌剤を水道水に使用する場合、水道水には塩素が含
まれているが、この銀担持抗菌剤の銀の担持量が多いた
めにその効力に問題はない。The method of supporting silver on the synthetic zeolite of fine particles is stopped, and as shown in the Examples, silver is directly applied to zeolite particles having a size that can be used as an antibacterial agent for water treatment or molded zeolite particles. Was attempted to be carried. A natural zeolite crushed product as a carrier carrying silver, A
Zeolite rod-shaped molded product (diameter 1.5 mm), A-type zeolite coin-shaped molded product (diameter 25 mm, thickness 2-3 m)
m) and other mullite molded articles having a certain size. Good results were obtained for all of these samples. That is, It became. As for the A-type zeolite-based molded rod, the column elution test, the adjustment test of the silver elution concentration, and the long-term elution test using a beaker were performed with tap water using SV5 and SV20. It was confirmed.
Natural zeolites are abundant in Japan and inexpensive. However, the amount of silver supported is limited to 5 mg-Ag / g-Z, and has not been successful as an antibacterial agent. However, when the raw rock of the mordenite natural zeolite produced in Fukushima Prefecture was crushed and silver was supported by the method of the present invention, 145 mg of Ag was supported per g of zeolite. Furthermore, a column elution test was performed using these silver zeolites, and as a result of preparing three groups of columns and testing the elution of silver and the adjustment of the silver elution concentration, natural zeolite carrying silver was synthesized as an antibacterial agent for water treatment. It is considered that there is a standard that can be used together with the A-type zeolite-based molded product. Further, since the manufacturing process is significantly simplified, the production cost can be reduced. A-type zeolite has a high concentration of aluminum contained in the crystal lattice, a high ion exchange capacity, and a high silver-carrying capacity, but has a low acid resistance, and its crystal structure collapses when immersed in a solution having a pH of 5 or less. Therefore, an important feature of the method for producing the silver-supported zeolite as the antibacterial agent for water treatment of the present invention is that the concentration of the silver-supporting treatment solution is kept at pH 5 or less and the amount of the aqueous solution per 1 g of zeolite is reduced. That is, the amount was extremely increased. Hereinafter, a comparison with the conventional product is shown. As described above, as a result of extremely increasing the amount of the aqueous solution per 1 g of zeolite, the concentration of the processing solution for supporting silver was not reduced to PH5 or less, and the amount of silver supported per 1 g of zeolite and per 1 g of zeolite were reduced. The weight percent of supported silver was as described above. When the silver-supported antibacterial agent for water treatment of the present invention is used in tap water, the tap water contains chlorine, but there is no problem in its efficacy because the silver-supported antibacterial agent has a large amount of silver carried. .
【0006】[0006]
【実施例1】天然ゼオライト原岩の銀の吸着試験につい
て説明する。 福島県産モルデナイト系天然ゼオライト
の原岩を破砕して篩により粒径を1.68〜2.00m
mとし、銀の吸着等温線を作成した。試料を水洗、乾
燥、脱気等の前処理の後、200mlビーカーに移し、
所定濃度の硝酸銀を加え、これを室温で1時間振とうし
た後、孔径0.45μのメンブランフィルターでろ過
し、ろ液中の銀濃度をグラファイト炉原子吸光法で定量
した。これによって図1の銀の吸着等温線が作成でき
た。図1に示すように、銀の濃度が150〜2500m
g/Lの範囲で銀の吸着は8.0〜90mg−Ag/g
−Zとなった。こうして天然ゼオライトへの銀の担持特
性を確認することができた。Example 1 A description will be given of a silver adsorption test of a natural zeolite raw rock. The raw rock of mordenite natural zeolite from Fukushima Prefecture is crushed and the particle size is 1.68 to 2.00 m using a sieve.
m and a silver adsorption isotherm was created. After pretreatment such as washing, drying and degassing, the sample is transferred to a 200 ml beaker,
After adding silver nitrate at a predetermined concentration and shaking at room temperature for 1 hour, the mixture was filtered through a membrane filter having a pore size of 0.45 μm, and the silver concentration in the filtrate was quantified by graphite furnace atomic absorption spectrometry. Thereby, the adsorption isotherm of silver of FIG. 1 was created. As shown in FIG. 1, the silver concentration is 150 to 2500 m.
In the range of g / L, the adsorption of silver is 8.0 to 90 mg-Ag / g.
-Z. Thus, the characteristics of supporting silver on natural zeolite could be confirmed.
【0007】[0007]
【実施例2】次に、銀を担持した天然ゼオライトからの
銀の溶出試験について説明する。銀の抗菌性について
は、例えば大腸菌の場合5.0μg/L以上で明確な効
果があることや、また安全性については米国の水道水の
基準が50μg/L以下とされていることを考慮する
と、実用上は銀の溶出濃度の調整が必要となる。そこで
吸着等温線作成法に準じて銀の担持量が56および14
5mg−Ag/g−Zeoliteのカラム溶出試験用
の銀担持天然ゼオライトを作成し、これらの銀担持ゼオ
ライトと銀無担持ゼオライトとを用いて図2に示すよう
な3種類のカラムを作成し銀の溶出試験を行った。この
時、内径15.5mmのガラス製カラムを使用し、それ
に銀担持天然ゼオライトを入れ、上部からSV5でイオ
ン交換水を流下させ、流出液中の銀濃度をグラファイト
炉原子吸光法で定量した。その結果を図2に示す。銀5
6mg担持ゼオライト層高20cmだけのカラム1で
は、銀の溶出濃度は2.5〜5.5mg/Lの範囲であ
るが、カラムの上部に銀145mg担持ゼオライト層高
2cmの下に無担持ゼオライト層高18cmを充填させ
たカラム2では、溶出濃度は0.05〜0.3mg/L
となり、さらにカラムの上部に銀145mg担持ゼオラ
イト層高2cmの下に無担持ゼオライト層高36cmを
充填させたカラム3では、溶出濃度は0.01〜0.0
6mg/Lとなった。このように、銀担持天然ゼオライ
トの下に無担持天然ゼオライトを配すると、銀の溶出濃
度を調節できることが分かり、抗菌剤として利用できる
ことが確認された。Example 2 Next, a description will be given of a test for elution of silver from a natural zeolite carrying silver. Considering the antibacterial properties of silver, for example, in the case of Escherichia coli, there is a clear effect at 5.0 μg / L or more, and regarding the safety, considering that the US tap water standard is 50 μg / L or less. In practice, it is necessary to adjust the silver elution concentration. Therefore, according to the adsorption isotherm preparation method, the supported amount of silver was 56 and 14
A silver-supported natural zeolite for column elution test of 5 mg-Ag / g-Zeolite was prepared, and three types of columns as shown in FIG. 2 were prepared using these silver-supported zeolite and silver-free zeolite to prepare silver. A dissolution test was performed. At this time, a glass column having an inner diameter of 15.5 mm was used, silver-loaded natural zeolite was put into the column, ion-exchanged water was allowed to flow down from above with SV5, and the silver concentration in the effluent was quantified by graphite furnace atomic absorption spectrometry. The result is shown in FIG. Silver 5
In column 1 having a 6 mg-supported zeolite layer height of only 20 cm, the elution concentration of silver is in the range of 2.5 to 5.5 mg / L, but the unsupported zeolite layer is located below the 145 mg silver-supported zeolite layer height of 2 cm above the column. In column 2 packed at a height of 18 cm, the elution concentration is 0.05 to 0.3 mg / L.
Further, in column 3 in which an unsupported zeolite layer height of 36 cm was packed under a 145 mg silver-supported zeolite layer height of 2 cm at the top of the column, the elution concentration was 0.01 to 0.0
It became 6 mg / L. Thus, it was found that when the non-supported natural zeolite was placed under the silver-supported natural zeolite, the elution concentration of silver could be adjusted, and it was confirmed that it could be used as an antibacterial agent.
【0008】[0008]
【実施例3】合成A型ゼオライト成形品(棒状 径1.
5mm)の銀の担持について説明する。合成A型ゼオラ
イト成形品はA4型ゼオライト60%に木節粘土30
%、ベントナイト10%を混合し、これに糊(CMC2
%溶液)を加えて混練りし、径1.5mmの棒状に押出
し成形し、風乾し、その後600°Cで3時間焼成して
作ったものである。このA型ゼオライト成形品につい
て、所定濃度の硝酸銀で処理した後、銀の濃度が100
〜5000mg/Lの範囲で銀の吸着は19.76〜4
80mg−Ag/g−Zとなった。図3に示すようにこ
の銀の吸着等温線によってA型ゼオライト成形品に対す
る銀の担持特性を確認することができた。さらにこの吸
着等温線の作成法に準じて銀の担持量が533.0mg
−Ag/g−Zの試料を得た。Example 3 Synthetic A-type zeolite molded product (rod-shaped diameter 1.
5 mm) of silver will be described. Synthetic A type zeolite molded product is A4 type zeolite 60% and Kibushi clay 30
% And bentonite 10%, and paste (CMC2
% Solution), kneaded, extruded into a rod having a diameter of 1.5 mm, air-dried, and then fired at 600 ° C. for 3 hours. After treating this type A zeolite molded article with silver nitrate at a predetermined concentration, the silver concentration becomes 100%.
Silver adsorption is 19.76-4 in the range of -5000 mg / L.
It became 80 mg-Ag / g-Z. As shown in FIG. 3, the silver adsorption characteristic on the A-type zeolite molded article could be confirmed from the adsorption isotherm of silver. Further, according to the method of preparing the adsorption isotherm, the amount of silver carried was 533.0 mg.
-Ag / g-Z sample was obtained.
【0009】[0009]
【実施例4】次に 実施例3の合成A型ゼオライト成形
品からの銀の溶出試験について説明する。内径15.5
mmのガラス製カラムに銀を担持した試料(533.0
mg−Ag/g−Z)を上層に2.5cm、銀無担持ゼ
オライト(A型成形ゼオライト)をその下層に36cm
充填しカラムを組み立て、上部からSV5で水道水を流
下させた。カラムより流下した水道水中の銀濃度をグラ
ファイト炉原子吸光法で定量した。カラムを通過した水
道水は循環させなかった。溶出時間は126時間、通過
した水道水は17.29リットル、ほぼ2時間おきに試
料を採取した。最初から28時間に至る間、溶出した銀
の濃度は300〜450ppbの範囲を示した。30時
間以降最後までの間、溶出した銀の濃度はほぼ200p
pbで平衡していることを示した。銀担持試料の銀は極
めて高濃度のものであるが、このような二層構造のカラ
ムによって溶出する銀の濃度を調節できることが確認さ
れた。ちなみに水道水のイオンクロマトグラフ法による
分析結果は次の通りである。 なお、水道水は PH7.86(15.7℃) μs/cm 225EXAMPLE 4 Next, a description will be given of a test for elution of silver from the synthetic A-type zeolite molded product of Example 3. Inner diameter 15.5
sample supporting silver on a 50 mm glass column (533.0).
mg-Ag / g-Z) in an upper layer of 2.5 cm, and a silver-free zeolite (A-type zeolite) in a lower layer of 36 cm.
The column was packed and assembled, and tap water was allowed to flow down from above with SV5. Silver concentration in tap water flowing down from the column was determined by graphite furnace atomic absorption spectrometry. Tap water that passed through the column was not circulated. Elution time was 126 hours, passed tap water was 17.29 liters, and samples were collected almost every two hours. During the first 28 hours, the eluted silver concentration ranged from 300 to 450 ppb. From 30 hours to the end, the concentration of eluted silver is almost 200 p.
It showed equilibrium in pb. Although the silver in the silver-carrying sample had an extremely high concentration, it was confirmed that the concentration of the eluted silver could be adjusted by such a two-layered column. Incidentally, the analysis results of tap water by ion chromatography are as follows. Tap water is PH 7.86 (15.7 ° C) μs / cm 225
【0010】[0010]
【実施例5】この実施例は実施例4の銀の溶出試験より
もっと厳しい条件での溶出試験であって、実際の操業の
場を前提として行った。カラムの構成は銀担持と銀無担
持との組み合わせとせず、銀担持ゼオライトのみとし、
試料は418mg−Ag/g−Zeoliteで層高を
6cm(11.3cm3)とした。またSVを20とし
た(3.8ml/min)。水道水を使用し、延べ12
7時間試験した。通過した水道水は17596mlであ
った。溶出した銀の濃度は、サンプリング18回中、 20〜29ppmを示した回数 7回 19ppm以下 を示した回数 6回 30〜36ppmを示した回数 5回 となった。なお、銀の溶出量は測定区画毎の銀の濃度
(mg/L)と通過水量Lから求めて 415.5m
g、銀担持試料の銀含有量は4180mg(418mg
−Ag/g−Zeolite×10g)であるので、銀
担持試料の含有する銀の量の約10%が溶出したことを
示す結果となった。Example 5 This example is a dissolution test under more severe conditions than the dissolution test of silver of Example 4, and was performed on the premise of an actual operation. The configuration of the column was not a combination of silver-carrying and silver-non-carrying, only silver-carrying zeolite,
The sample was 418 mg-Ag / g-Zeolite and the layer height was 6 cm (11.3 cm 3 ). The SV was set to 20 (3.8 ml / min). Use tap water for a total of 12
Tested for 7 hours. The amount of tap water passed was 17596 ml. The concentration of eluted silver was 20 times to 29 ppm out of 18 times, 7 times 19 ppm or less, 6 times 30 to 36 ppm, and 5 times. The amount of silver eluted was 415.5 m calculated from the silver concentration (mg / L) and the amount of passing water L in each measurement section.
g, the silver content of the silver-carrying sample was 4180 mg (418 mg
-Ag / g-Zeolite × 10 g), which indicated that about 10% of the amount of silver contained in the silver-supported sample was eluted.
【0011】[0011]
【実施例6】銀担持A型ゼオライト成形品の水道水中に
おける長時間の溶出試験を行った。 1)銀担持A型ゼオライト成形品を使用( 銀担持量
418mg−Ag/g−Zeolite) 2)使用量 1g 3)水道水 1000ml 一定時間経過して新しい水
道水と入れ替えた 4)マグネティック スターラで撹拌 5)撹拌時間累計 1848 時間 以上から 1848 時間に亘りそのつど水道水100
0ml ずつ取り替え、撹拌を続けたが、当初第1回目
と第2回目は立ち上がり時、銀担持粒子の表層から多め
の銀が剥離し高濃度の溶出となったが、第3回以降の銀
の溶出は撹拌をやめた1848時間まで安定した濃度を
示すことが確かめられた。また溶出試験を終了するころ
になっても銀の溶出は衰えず、水道水中でこの銀担持抗
菌剤は少量で長時間使用できることが確認できた。Example 6 A long-term dissolution test of a silver-supported A-type zeolite molded product in tap water was performed. 1) Using a silver-supported A-type zeolite molded product (silver supported amount)
418mg-Ag / g-Zeolite) 2) Usage amount 1g 3) Tap water 1000ml Replaced with fresh tap water after a certain period of time 4) Stir with magnetic stirrer 5) Total stirring time 1848 hours From the above, tap water 100 for 1848 hours
The mixture was replaced by 0 ml at a time and stirring was continued. Initially, at the first and second starts, a large amount of silver was peeled off from the surface layer of the silver-supported particles, resulting in high-concentration elution. It was confirmed that the elution showed a stable concentration until 1848 hours when the stirring was stopped. In addition, even when the dissolution test was completed, the dissolution of silver did not deteriorate, confirming that the silver-carrying antibacterial agent could be used in tap water for a long time with a small amount.
【0012】[0012]
【実施例7】A型ゼオライトを出発原料としてコイン状
薄片成形品(径25mm、厚さ2〜3mm)を焼成し
た。これについての焼成温度別の銀担持試験を行った。 焼成温度は低いと製品の強度が弱くなり、高温になると
ゼオライトの骨格構造が壊れれてしまう。この試験の結
果、焼成温度は600〜640°Cが好ましく、溶液1
リットル当りの銀 Agの量は2500mg前後の時、
好ましい結果が得られることが分かった。上の表から成
形体1g当りの銀担持は128.23mgから418.
58mgの範囲にあり、ゼオライト1g当りの最大銀担
持重量パーセントは41.86%(試料番号5)であ
る。EXAMPLE 7 A coin-shaped flake (diameter 25 mm, thickness 2-3 mm) was fired using A-type zeolite as a starting material. A silver loading test was carried out for each of the firing temperatures. If the firing temperature is low, the strength of the product is weakened, and if the firing temperature is high, the framework structure of zeolite is broken. As a result of this test, the firing temperature is preferably from 600 to 640 ° C.
When the amount of Ag per liter is around 2500mg,
It has been found that favorable results are obtained. From the table above, the amount of silver carried per gram of the molded product was from 128.23 mg to 418.
It is in the range of 58 mg, with a maximum silver loading weight percent per gram of zeolite of 41.86% (sample no. 5).
【0013】[0013]
【効果】本発明は、現在行われている製法、即ち、まづ
銀ゼオライトを作り、これをバインダに加え、或いは合
成樹脂に混合して成形するといった従来の方法によらな
いで、水処理用として使用できるような粒子の大きなゼ
オライトの成形品、或いは天然ゼオライトの破砕したも
のに対して直接、簡単に銀の担持を行うので製造工程が
著しく簡素化され、その結果生産コストを安価にし、同
時に従来の製品よりはるかに性能が優れた水処理用抗菌
剤を作ることができる効果がある。本発明はまた、ゼオ
ライト又はゼオライト系加工品に限らず耐火粘度ムライ
ト又はムライト系加工品にも同様に直接銀の担持が可能
である。本発明はまた、ゼオライトに対する水溶液の量
を従来のものより極度に増量した結果、銀担持用処理液
の濃度をPH5以下に落とすことがないのでゼオライト
の結晶構造を崩壊させることがなく、同時にゼオライト
に対する銀の高担持量を実現できる効果がある。また、
本発明により担体に銀を担持させた銀担持材のみで使用
することもできるが、銀担持材と銀を担持していない銀
無担持材との自在な組み合わせによって銀の溶出濃度の
調節を可能とする効果がある。本発明による水処理用銀
担持抗菌剤は、飲料水やプール、浄水場、冷却塔、水溶
性油剤、浴場水、振とう式加湿器等に使用して殺菌、防
黴効果があり、特にレジオネラ症の予防や、冷却塔にお
いては藻の抑制、スライム除去、機械冷却回路における
目詰まり防止、水溶性油剤の腐敗防止、悪臭対策など広
範囲の水処理用として使用できる。According to the present invention, there is provided a method for water treatment, which does not use a conventional method of producing silver zeolite, adding it to a binder, or mixing it with a synthetic resin and molding it. Since silver is directly and easily supported on a zeolite molded article having a large particle size or a crushed natural zeolite, the production process is significantly simplified, and as a result, the production cost is reduced, and There is an effect that an antibacterial agent for water treatment having much higher performance than conventional products can be produced. In the present invention, silver can be directly supported not only on a zeolite or a zeolite-based processed product but also on a refractory viscosity mullite or a mullite-based processed product. According to the present invention, the amount of the aqueous solution with respect to the zeolite is extremely increased as compared with the conventional one. As a result, the concentration of the processing solution for supporting silver does not drop to PH5 or less, so that the crystal structure of the zeolite does not collapse, and at the same time, the zeolite does not collapse. This has the effect of realizing a high amount of silver supported on silver. Also,
According to the present invention, it is possible to use only a silver-carrying material having silver supported on a carrier, but it is possible to adjust the silver elution concentration by a free combination of a silver-carrying material and a silver-free material not carrying silver. Has the effect. The silver-supported antibacterial agent for water treatment according to the present invention has a bactericidal and fungicidal effect when used in drinking water, pools, water purification plants, cooling towers, water-soluble oils, bath water, shaking humidifiers, etc., especially Legionella. It can be used for a wide range of water treatments such as prevention of diseases, suppression of algae in cooling towers, removal of slime, prevention of clogging in mechanical cooling circuits, prevention of decay of water-soluble oils, and countermeasures against odors.
【図1】天然ゼオライト原岩の破砕粒( 1.68〜
2.00mm)の銀の吸着等温線を示すグラフである。Fig. 1 Crushed granules of natural zeolite raw rock (1.68 ~
2.00 mm) is a graph showing an adsorption isotherm of silver.
【図2】図1の天然ゼオライトの破砕粒に銀を担持した
担持ゼオライトのみのカラム1と銀担持ゼオライトと銀
無担持ゼオライトとを組み合わせたカラム2とカラム3
の3種類のカラムを作成して銀の溶出試験を行った時の
銀の溶出状態を示すグラフである。 ○印 銀56mg坦持ゼオライト層高20cmの場合
(カラム1) △印 銀145mg坦持ゼオライト層高2cmの下に無
坦持ゼオライト層高18cmの場合(カラム2) □印 銀145mg坦持ゼオライト層高2cmの下に無
坦持ゼオライト層高36cmの場合(カラム3)FIG. 2 is a column 1 of only supported zeolite in which crushed natural zeolite particles of FIG. 1 support silver, and columns 2 and 3 in which silver-supported zeolite and silver-free zeolite are combined.
3 is a graph showing the elution state of silver when three types of columns were prepared and a silver elution test was performed. ○ In the case of a zeolite layer carrying 56 mg of silver and 20 cm in height (column 1) △ In the case of a zeolite layer carrying no zeolite and a height of 18 cm below a height of 2 cm of the zeolite carrying 145 mg of silver (column 2) □ A zeolite layer carrying 145 mg of silver When the unsupported zeolite layer height is 36 cm below the height of 2 cm (column 3)
【図3】A型ゼオライト成形品の銀の吸着等温線を示す
グラフである。FIG. 3 is a graph showing an adsorption isotherm of silver of a molded product of type A zeolite.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 1/50 540 C02F 1/50 540E 540F ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C02F 1/50 540 C02F 1/50 540E 540F
Claims (2)
さのゼオライト粒子又はゼオライト系加工品に、ゼオラ
イトの結晶構造を破壊しない程度のPHを示す処理液中
で直接銀を担持させてなる水処理用銀担持抗菌剤。1. Zeolite particles or zeolite-based processed products of an arbitrary size capable of solid-liquid separation for water treatment are directly supported with silver in a treatment liquid having a pH that does not destroy the crystal structure of zeolite. Silver carrying antibacterial agent for water treatment.
さのゼオライト粒子又はゼオライト系加工品に、ゼオラ
イトの結晶構造を破壊しない程度のPHを示す処理液中
で直接銀を担持させた銀担持材のみで、又は銀担持材と
銀無担持材との組み合わせによって銀の溶出濃度の調節
を可能としてなる水処理用銀担持抗菌剤の使用方法。2. Zeolite particles or zeolite-based processed products of any size capable of solid-liquid separation for water treatment are directly supported with silver in a treatment solution having a pH that does not destroy the crystal structure of zeolite. A method of using a silver-carrying antibacterial agent for water treatment, which makes it possible to adjust the elution concentration of silver using only a silver-carrying material or a combination of a silver-carrying material and a silver-free material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000132952A JP2001278715A (en) | 2000-03-29 | 2000-03-29 | Silver-supporting antimicrobial agent for water treatment and its application method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000132952A JP2001278715A (en) | 2000-03-29 | 2000-03-29 | Silver-supporting antimicrobial agent for water treatment and its application method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2001278715A true JP2001278715A (en) | 2001-10-10 |
Family
ID=18641547
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000132952A Pending JP2001278715A (en) | 2000-03-29 | 2000-03-29 | Silver-supporting antimicrobial agent for water treatment and its application method |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100503462C (en) * | 2007-07-13 | 2009-06-24 | 赵晓斌 | Algae treatment agent and method of use thereof |
| JP2012149050A (en) * | 2010-12-27 | 2012-08-09 | Kenji Nakamura | Antimicrobial pack sheet package |
| CN103449577A (en) * | 2013-09-16 | 2013-12-18 | 湖南大学 | Method for efficiently and quickly killing bacteria in water |
| WO2015098762A1 (en) * | 2013-12-25 | 2015-07-02 | ニッカウヰスキー株式会社 | Device and method for removing unwanted component included in beverage |
| CN109095945A (en) * | 2018-08-29 | 2018-12-28 | 佛山市森昂生物科技有限公司 | A kind of preparation method of antibacterial mould-proof-type zeolite keynote wet stock |
-
2000
- 2000-03-29 JP JP2000132952A patent/JP2001278715A/en active Pending
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100503462C (en) * | 2007-07-13 | 2009-06-24 | 赵晓斌 | Algae treatment agent and method of use thereof |
| JP2012149050A (en) * | 2010-12-27 | 2012-08-09 | Kenji Nakamura | Antimicrobial pack sheet package |
| CN103449577A (en) * | 2013-09-16 | 2013-12-18 | 湖南大学 | Method for efficiently and quickly killing bacteria in water |
| WO2015098762A1 (en) * | 2013-12-25 | 2015-07-02 | ニッカウヰスキー株式会社 | Device and method for removing unwanted component included in beverage |
| JPWO2015098762A1 (en) * | 2013-12-25 | 2017-03-23 | ニッカウヰスキー株式会社 | Method and apparatus for removing unnecessary components contained in beverage |
| US11028353B2 (en) | 2013-12-25 | 2021-06-08 | The Nikka Whisky Distilling Co., Ltd. | Method for removing unwanted component included in beverage |
| CN109095945A (en) * | 2018-08-29 | 2018-12-28 | 佛山市森昂生物科技有限公司 | A kind of preparation method of antibacterial mould-proof-type zeolite keynote wet stock |
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